CN101092360A - Method for catalyzing and synthesizing tri-butyl citrate from methylal naphthalene sulfonic acid - Google Patents

Method for catalyzing and synthesizing tri-butyl citrate from methylal naphthalene sulfonic acid Download PDF

Info

Publication number
CN101092360A
CN101092360A CNA2007100433737A CN200710043373A CN101092360A CN 101092360 A CN101092360 A CN 101092360A CN A2007100433737 A CNA2007100433737 A CN A2007100433737A CN 200710043373 A CN200710043373 A CN 200710043373A CN 101092360 A CN101092360 A CN 101092360A
Authority
CN
China
Prior art keywords
sulfonic acid
methylal
naphthene sulfonic
water
reaction
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CNA2007100433737A
Other languages
Chinese (zh)
Other versions
CN101092360B (en
Inventor
杨建国
高珊
梁学正
王有菲
龚国珍
何鸣元
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
East China Normal University
Original Assignee
East China Normal University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by East China Normal University filed Critical East China Normal University
Priority to CN200710043373A priority Critical patent/CN101092360B/en
Publication of CN101092360A publication Critical patent/CN101092360A/en
Application granted granted Critical
Publication of CN101092360B publication Critical patent/CN101092360B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/582Recycling of unreacted starting or intermediate materials

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

This invention discloses a method for catalytically synthesizing tributyl citrate by using naphthalenesulfonic acid/formaldehyde condensation compound as the catalyst by ester synthesis. The method comprises: performing ester synthesis by using naphthalenesulfonic acid/formaldehyde condensation compound as the catalyst, filtering after reaction, and vacuum-distilling to obtain tributyl citrate. The method has such advantages as high yield (94.4-99%), low catalyst consumption (0.37-1.85 wt. % of raw materials), mild reaction conditions, short reaction time, recoverable catalyst, and no need for toxic toluene solvent. Reactant n-butanol can be directly used as the water-carrying agent.

Description

A kind of method with naphthene sulfonic acid methylal catalysis synthesizing citric acid tri-n-butyl
Technical field
The present invention relates to the organic chemistry synthesis technical field, specifically a kind of method with naphthene sulfonic acid methylal catalysis synthesizing citric acid tri-n-butyl.
Background technology
Tributyl citrate is nonpoisonous and tasteless " green " environmentally-friendly plastic softening agent, be widely used in food and medical instrumentation package, makeup, daily necessities, toy, military supplies etc., have that consistency is good, plasticizing efficiency is high, nontoxic, easily by advantage such as biological degradation and volatility be little, winter hardiness, photostabilization and have excellent water-resistance, and mould resistance is arranged in resin, do not grow mould.The shared goods hardness that improves of tributyl citrate and other non-toxic plasticizers, especially more suitable to soft fiber ether.Simultaneously, tool improves the nitrocotton anti-uv-ray, and is the solvent of multiple spices, also can be used for the defoamer of protein-based solution.Therefore, tributyl citrate becomes present conventional plasticizers phthalate " green " substitute.The traditional method of synthesizing citric acid tri-n-butyl is to do catalyzer [Song Qihuang chief editor with the vitriol oil, fine chemistry industry technology, Beijing: Chemical Industry Press, 1995:95], this catalyzer exists side reaction many, refining difficulty, equipment corrosion is serious, and the aftertreatment complexity produces industry " three wastes ", shortcomings such as contaminate environment, its application have been subjected to very big restriction.Some catalyzer that grew up afterwards all have catalytic activity preferably as being catalyzer [Xie Wenlei etc., Speciality Petrochemicals, 1998, (4): 7-9] with the tosic acid to this reaction, but catalyzer costs an arm and a leg, and can not recirculation use.
Summary of the invention
The objective of the invention is provides a kind of eco-friendly, economic heterogeneous catalysis to prepare the method for tributyl citrate at the deficiencies in the prior art, is that catalyzer solves the existing problem of prior art with the naphthene sulfonic acid methylal.
The present invention solves this technical problem by the following technical programs: be catalyzer with the naphthene sulfonic acid methylal in the ester building-up process, after reaction finishes, filter, filtrate is handled through normal pressure, underpressure distillation can obtain tributyl citrate, the naphthene sulfonic acid methylal that reaction end after-filtration goes out can be recycled, and activity remains unchanged substantially.
Reaction expression of the present invention is as follows:
Figure A20071004337300041
The present invention includes following concrete steps:
The preparation of the 1st step naphthene sulfonic acid methylal
5~20g naphthalene is heated to 160 ℃, the vitriol oil of slow Dropwise 5~20ml behind 120~160 ℃ of following heated and stirred 1~6h, is cooled to 90~120 ℃ more then, after adding 2~5ml water, drip formaldehyde solution 10~20ml, keep 100 ℃ of heating 4~8h, get black solid, adding boiling water then washs, suction filtration, 100~140 ℃ of oven dry get the naphthene sulfonic acid methylal;
The 2nd step esterification
In having the 100mL three-necked bottle of induction stirring, thermometer, reflux condensing tube, water trap, add 0.1~0.15mol citric acid, 0.4~0.6mol propyl carbinol and 0.1~0.5g naphthene sulfonic acid methylal, reflux stirs, the water that reaction is produced is told from water trap, reaction to the anhydrous water trap that enters again stops, and gets the thick product of tributyl citrate;
The separation of the 3rd step catalyzer and the purifying of product
Thick product is filtered, and the naphthene sulfonic acid methylal that leaches is directly used in down secondary response, and filtrate is reclaimed excessive propyl carbinol through the normal pressure distillation, be cooled to room temperature then, underpressure distillation, the cut of 178~180 ℃/400Pa of collection obtains water white product tributyl citrate.
Described naphthene sulfonic acid methylal consumption accounts for 0.37~1.85% of reaction raw materials gross weight.
Compared with prior art, advantage of the present invention is: (1) productive rate height is up to 99.0%; (2) catalyzer is cheap, and catalyst levels is little, accounts for 0.37~1.85% of reaction raw materials gross weight; (3) reaction conditions gentleness, the reaction times is short; (4) catalyzer can be recycled; (5) directly make the band aqua, avoided using deleterious toluene etc. with the reactant propyl carbinol.
Embodiment
Below will the present invention is further elaborated by specific embodiment:
Embodiment 1
The preparation of the 1st step naphthene sulfonic acid methylal:
The 5g naphthalene is heated to 160 ℃, slowly drips the vitriol oil of 15ml then, behind 140 ℃ of following heated and stirred 4h, be cooled to 100 ℃ again, behind the adding 2ml water, drip formaldehyde solution 15ml, keep 100 ℃ of heating 5h, get black solid.Add boiling water then and wash, suction filtration, 110 ℃ of oven dry get the naphthene sulfonic acid methylal;
The 2nd step esterification
In having the 100ml three-necked bottle of induction stirring, thermometer, reflux condensing tube, water trap, add 0.1mol citric acid, 0.45mol propyl carbinol and 0.3g naphthene sulfonic acid methylal, reflux stirs, the water that reaction is produced is told from water trap, reaction to the anhydrous water trap that enters again stops, and gets the thick product of tributyl citrate;
The separation of the 3rd step catalyzer and the purifying of product
Thick product is filtered, and the naphthene sulfonic acid methylal that leaches is directly used in down secondary response, and filtrate is reclaimed excessive propyl carbinol through the normal pressure distillation, is cooled to room temperature then, underpressure distillation, and the cut of 178~180 ℃/400Pa of collection gets water white transparency product tributyl citrate.Productive rate is 99.0%.
Embodiment 2-4
Except for the following differences, all the other are identical with embodiment 1, are 0.3g at naphthene sulfonic acid methylal consumption, and the citric acid consumption is 0.1mol, and the propyl carbinol consumption the results are shown in Table 1 to the influence of reaction.
Table 1
Embodiment Acid alcohol is than (mole) Productive rate/%
2 3 4 1∶4.0 1∶5.0 1∶6.0 98.2 98.9 98.6
Embodiment 5-8
Except for the following differences, all the other are identical with embodiment 1, and naphthene sulfonic acid methylal consumption the results are shown in Table 2 to the influence of reaction
Table 2
Embodiment Catalyst levels/g Productive rate/%
5 6 7 8 0.1 0.2 0.3 0.5 97.3 98.4 99.0 98.5
Embodiment 9-12
Except for the following differences, all the other are identical with embodiment 1, and catalyst recirculation uses the influence to reaction to the results are shown in Table 3
Table 3
Embodiment The catalyst recirculation access times Productive rate/%
9 10 11 12 1 2 3 4 98.9 97.8 96.9 94.4

Claims (2)

1, a kind of method with naphthene sulfonic acid methylal catalysis synthesizing citric acid tri-n-butyl is characterized in that: make catalyzer with the naphthene sulfonic acid methylal in the ester building-up process, after filtration, gained filtrate promptly obtained tributyl citrate through underpressure distillation after reaction finished; Its concrete steps are:
The preparation of the 1st step naphthene sulfonic acid methylal
5~20g naphthalene is heated to 160 ℃, the vitriol oil of slow Dropwise 5~20ml behind 120~160 ℃ of following heated and stirred 1~6h, is cooled to 90~120 ℃ more then, after adding 2~5ml water, drip formaldehyde solution 10~20ml, keep 100 ℃ of heating 4~8h, get black solid, adding boiling water then washs, suction filtration, 100~140 ℃ of oven dry get the naphthene sulfonic acid methylal;
The 2nd step esterification
In having the 100mL three-necked bottle of induction stirring, thermometer, reflux condensing tube, water trap, add 0.1~0.15mol citric acid, 0.4~0.6mol propyl carbinol and 0.1~0.5g naphthene sulfonic acid methylal, reflux stirs, the water that reaction is produced is told from water trap, reaction to the anhydrous water trap that enters again stops, and gets the thick product of tributyl citrate;
The separation of the 3rd step catalyzer and the purifying of product
Thick product is filtered, and the naphthene sulfonic acid methylal that leaches is directly used in down secondary response, and filtrate is reclaimed excessive propyl carbinol through the normal pressure distillation, be cooled to room temperature then, underpressure distillation, the cut of 178~180 ℃/400Pa of collection obtains water white product tributyl citrate.
2, method according to claim 1 is characterized in that described naphthene sulfonic acid methylal consumption accounts for 0.37~1.85% of reaction raw materials gross weight.
CN200710043373A 2007-07-03 2007-07-03 Method for catalyzing and synthesizing tri-butyl citrate from methylal naphthalene sulfonic acid Expired - Fee Related CN101092360B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN200710043373A CN101092360B (en) 2007-07-03 2007-07-03 Method for catalyzing and synthesizing tri-butyl citrate from methylal naphthalene sulfonic acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN200710043373A CN101092360B (en) 2007-07-03 2007-07-03 Method for catalyzing and synthesizing tri-butyl citrate from methylal naphthalene sulfonic acid

Publications (2)

Publication Number Publication Date
CN101092360A true CN101092360A (en) 2007-12-26
CN101092360B CN101092360B (en) 2010-05-19

Family

ID=38990821

Family Applications (1)

Application Number Title Priority Date Filing Date
CN200710043373A Expired - Fee Related CN101092360B (en) 2007-07-03 2007-07-03 Method for catalyzing and synthesizing tri-butyl citrate from methylal naphthalene sulfonic acid

Country Status (1)

Country Link
CN (1) CN101092360B (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101481309A (en) * 2008-08-30 2009-07-15 杜晓晗 Preparation of high molecular weight nontoxic plasticizer
CN101250105B (en) * 2008-03-28 2010-06-09 华东师范大学 Method for synthesizing bio-diesel by using p-toluenesulfonic acid formaldehyde condensation polymer
CN105669443A (en) * 2015-12-31 2016-06-15 江苏瑞佳化学有限公司 Method of preparing tributyl citrate with nano-scale intercalated hydrotalcite catalyst
CN110876959A (en) * 2019-12-09 2020-03-13 怀化学院 Solid carbon sulfonic acid catalyst and preparation method thereof, and tributyl citrate and preparation method thereof

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100513344C (en) * 2005-01-31 2009-07-15 花王株式会社 Process for producing a naphthalenesulfonate formaldehyde condensate

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101250105B (en) * 2008-03-28 2010-06-09 华东师范大学 Method for synthesizing bio-diesel by using p-toluenesulfonic acid formaldehyde condensation polymer
CN101481309A (en) * 2008-08-30 2009-07-15 杜晓晗 Preparation of high molecular weight nontoxic plasticizer
CN101481309B (en) * 2008-08-30 2013-12-11 健雄职业技术学院 Preparation of high molecular weight nontoxic plasticizer
CN105669443A (en) * 2015-12-31 2016-06-15 江苏瑞佳化学有限公司 Method of preparing tributyl citrate with nano-scale intercalated hydrotalcite catalyst
CN110876959A (en) * 2019-12-09 2020-03-13 怀化学院 Solid carbon sulfonic acid catalyst and preparation method thereof, and tributyl citrate and preparation method thereof

Also Published As

Publication number Publication date
CN101092360B (en) 2010-05-19

Similar Documents

Publication Publication Date Title
CN102070450B (en) Method for synthesizing tributyl citrate
CN102320970B (en) Method for preparing tributyl citrate by using modified cation exchange resin as catalyst
CN1422237A (en) Process for preparing cumene which is used in the preparation of phenol
CN100349849C (en) Method for preparing tributyl citrate using mesoporous molecular sieve as catalyst
CN101092360B (en) Method for catalyzing and synthesizing tri-butyl citrate from methylal naphthalene sulfonic acid
CN100372830C (en) Catalyzing synthesis of citric tributyl ester from carbon-base sulfoacid
CN102126953A (en) Preparation method of nonanal and methyl formylcaprylate
CN101245008A (en) Method for synthesizing trioctyl lemon acid
CN102229523B (en) Preparation method of 3-chloro-1,2-propanediol
CN109796303B (en) Preparation method of isoprene glycol
CN102304045A (en) Integrated process for synthesizing acetyl tributyl citrate (ATBC) from active carbon solid-carried sulphuric acid catalyst
CN102659592A (en) Method for synthesizing tributyl citrate by using resorcinol formaldehyde resin based solid acid as catalyst
CN111215138A (en) catalyst, preparation method and application of catalyst in preparation of β -isophorone
CN111423317B (en) Production device and method for synthesizing dihydro jasmone spice through solid acid catalysis
CN108218678A (en) The separation and refining method and device of polymethoxy dimethyl ether
CN1242970C (en) Preparation for acetal solid catalyst and use thereof
CN101585776B (en) Method for synthetizing N,N-diisopropylethylamine
CN101735055A (en) Method for producing plasticizer tirbutyl citrate
CN101239911A (en) Method for synthesizing tributyl acetcitrate
CN102701907B (en) Green method for preparing nopol
CN102285883B (en) Method for synthesizing tributyl citrate (TBC) by adopting composite ionic liquid catalyst
CN101391957B (en) Method for preparing tributyl citrate by using rare-earth salt binary complex type solid acid as catalyst
CN112961051A (en) Method for purifying methyl 3-methoxypropionate
CN105152938B (en) A kind of technique efficiently synthesizing secondary carbon primary amine N1923
CN101070276A (en) Process for preparing acrolein by glycerin dewatering

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20100519

Termination date: 20120703